EP3438132B1 - Procédé de production de cellulose fibreuse et cellulose fibreuse - Google Patents

Procédé de production de cellulose fibreuse et cellulose fibreuse Download PDF

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Publication number
EP3438132B1
EP3438132B1 EP17775442.1A EP17775442A EP3438132B1 EP 3438132 B1 EP3438132 B1 EP 3438132B1 EP 17775442 A EP17775442 A EP 17775442A EP 3438132 B1 EP3438132 B1 EP 3438132B1
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Prior art keywords
fibrous cellulose
phosphoric acid
cellulose
ultrafine fibrous
slurry
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EP17775442.1A
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German (de)
English (en)
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EP3438132A1 (fr
EP3438132A4 (fr
Inventor
Yuichi Noguchi
Ikue HOMMA
Yusuke Matsubara
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Oji Holdings Corp
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Oji Holdings Corp
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    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/16—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only modified by a particular after-treatment
    • D21H11/18—Highly hydrated, swollen or fibrillatable fibres
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B5/00—Preparation of cellulose esters of inorganic acids, e.g. phosphates
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B15/00—Preparation of other cellulose derivatives or modified cellulose, e.g. complexes
    • C08B15/005—Crosslinking of cellulose derivatives
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B15/00—Preparation of other cellulose derivatives or modified cellulose, e.g. complexes
    • C08B15/10—Crosslinking of cellulose
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L1/00—Compositions of cellulose, modified cellulose or cellulose derivatives
    • C08L1/08—Cellulose derivatives
    • C08L1/16—Esters of inorganic acids
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/02—Chemical or chemomechanical or chemothermomechanical pulp
    • D21H11/04—Kraft or sulfate pulp
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H15/00—Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution
    • D21H15/02—Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution characterised by configuration

Definitions

  • the present invention relates to a method for producing ultrafine fibrous cellulose, and ultrafine fibrous cellulose. Moreover, the present invention also relates to ultrafine fibrous cellulose-containing slurry and an ultrafine fibrous cellulose-containing sheet.
  • ultrafine fibrous cellulose which have a fiber diameter of 1 ⁇ m or less, is known as cellulose fibers.
  • Such ultrafine fibrous cellulose can be used as a raw material for constituting a sheet or a complex. It has been known that when the ultrafine fibrous cellulose is used, the contacts of fibers are significantly increased, and thus that the tensile strength of such a sheet or a complex is significantly improved. Moreover, the use of the ultrafine fibrous cellulose in a thickener or the like has also been considered.
  • Ultrafine fibrous cellulose can be produced by subjecting conventional cellulose fibers to a mechanical treatment.
  • Cellulose fibers strongly bind to one another via a hydrogen bond. Accordingly, when ultrafine fibrous cellulose is produced by simply performing a mechanical treatment on such cellulose fibers, enormous energy is required to obtain the ultrafine fibrous cellulose.
  • Patent Documents 1 and 2 disclose phosphorylated ultrafine fibrous cellulose, in which a phosphoric acid group forms an ester with a hydroxyl group of cellulose, and a method for producing such phosphorylated ultrafine fibrous cellulose.
  • Patent Document 2 proposes that a phosphoric acid group introduction step is carried out in the presence of urea, and that the amount of the phosphoric acid groups introduced is increased by carrying out the phosphoric acid group introduction step multiple times.
  • ultrafine fibrous cellulose having phosphoric acid groups is required to comprise as many phosphoric acid groups as possible.
  • ultrafine fibrous cellulose can preferably exhibit high viscosity, when it is processed into slurry.
  • the present inventors have conducted studies for the purpose of efficiently producing such ultrafine fibrous cellulose.
  • phosphorylated ultrafine fibrous cellulose in which the amount of phosphoric acid groups introduced is sufficiently large and the formation of crosslinked structures via such phosphoric acid group is at a small level, can be efficiently obtained by a method for producing phosphorylated ultrafine fibrous cellulose, comprising forming a predetermined amount of crosslinked structure via phosphoric acid groups introduced into cellulose, then hydrolyzing the crosslinked structure, and then performing a fibrillation treatment.
  • the present inventors have also found that when such phosphorylated ultrafine fibrous cellulose can exhibit high viscosity, when they are processed into slurry, thereby completing the present invention.
  • the present invention has the following configuration.
  • ultrafine fibrous cellulose having phosphoric acid groups which can exhibit high viscosity when they are processed into slurry, can be efficiently obtained.
  • Figure 1 is a graph showing the relationship between the amount of NaOH added dropwise to a fiber raw material having a phosphoric acid group and electrical conductivity.
  • the present invention relates to a method for producing fibrous cellulose having a fiber width of 1000 nm or less (also referred to as "ultrafine fibrous cellulose").
  • the method for producing fibrous cellulose of the present invention comprises a step (A) of introducing phosphoric acid groups into cellulose fibers to form crosslinked structures via the phosphoric acid groups, thereby obtaining crosslinked phosphorylated cellulose fibers, a step (B) of breaking some or all of the crosslinked structures to obtain crosslink-broken phosphorylated cellulose fibers, and a step (C) of performing a mechanical treatment on the crosslink-broken phosphorylated cellulose fibers to obtain fibrous cellulose having a fiber width of 1000 nm or less.
  • step (A) crosslinked structures in an amount of 0.05 mmol/g or more and 2.0 mmol/g or less are formed.
  • step (B) is a step of performing the hydrolysis of the crosslinked structures in an aqueous solvent with pH 3 or more at a temperature of 80°C or higher.
  • step (A) since the method for producing fibrous cellulose of the present invention has a step of forming crosslinked structures (step (A)), many phosphoric acid groups can be introduced into cellulose fibers. Moreover, as described above, since a crosslink-breaking step (step (B)) is performed under predetermined conditions according to the production method of the present invention, the polymerization degree of ultrafine fibrous cellulose can be kept high. Since the production method of the present invention has the aforementioned steps, ultrafine fibrous cellulose having phosphoric acid groups can be efficiently obtained with a high yield in the present invention.
  • the phosphorylated ultrafine fibrous cellulose obtained by the above-described production method comprise a sufficiently high amount of phosphoric acid groups introduced and a low level of crosslinked structure formation, fibrillation has been sufficiently carried out. Moreover, the phosphorylated ultrafine fibrous cellulose obtained by the production method of the present invention maintains a high polymerization degree. As such, the phosphorylated ultrafine fibrous cellulose can exhibit specific functions possessed by ultrafine fibrous cellulose. For example, when the ultrafine fibrous cellulose obtained by the production method of the present invention are processed into slurry, the slurry has high transparency and high viscosity. Furthermore, when the ultrafine fibrous cellulose obtained by the production method of the present invention are processed into a sheet, the sheet can exhibit excellent mechanical strength.
  • the sheet when the ultrafine fibrous cellulose obtained by the production method of the present invention are processed into a sheet, the sheet can exhibit excellent yellowing resistance. This is considered mainly because the amount of groups having a urethane bond introduced into the ultrafine fibrous cellulose obtained by the method for producing fibrous cellulose of the present invention is suppressed.
  • urea and/or a derivative thereof are used as a phosphorylating agent, as well as a compound having a phosphoric acid group.
  • a group having a urethane bond is introduced into cellulose.
  • the amount of groups having a urethane bond introduced can also be suppressed.
  • the amount of groups having a urethane bond introduced can be controlled by performing the step (B) under alkaline conditions in the production method of the present invention.
  • the ultrafine fibrous cellulose obtained in the present invention can also exhibit excellent yellowing resistance. For example, even in a case where the ultrafine fibrous cellulose of the present invention is processed into a sheet and the sheet is then heated, an increase in the yellowness (YI value) of the sheet is suppressed.
  • the step (A) is a step of introducing phosphoric acid groups into cellulose fibers to form crosslinked structures via the phosphoric acid groups, so as to obtain crosslinked phosphorylated cellulose fibers.
  • the step (A) is a step of obtaining crosslinked phosphorylated cellulose fibers, and in the crosslinked phosphorylated cellulose fibers, crosslinked structures in an amount of 0.05 mmol/g or more and 2.0 mmol/g or less are formed.
  • the step (A) is composed of two steps, namely, a step (a1) of introducing phosphoric acid groups into cellulose fibers, and a step (a2) of forming crosslinked structures via the phosphoric acid groups to obtain crosslinked phosphorylated cellulose fibers, and also, the heat treatment step in the step (a1) of introducing phosphoric acid groups may serve both as a step (a1) and as a step (a2).
  • the step (a1) of introducing phosphoric acid groups into cellulose fibers can be carried out by allowing a fiber raw material comprising cellulose to react with at least one selected from a compound having a phosphoric acid group and a salt thereof (hereinafter, referred to as a "phosphorylating reagent" or "compound A").
  • a phosphorylating reagent may be mixed into the fiber raw material that is in a dry or wet state, in the form of a powder or a solution.
  • a powder or a solution of the phosphorylating reagent may be added into slurry of the fiber raw material.
  • the phosphoric acid group introduction step is performed by allowing at least one selected from a compound having a phosphoric acid group and a salt thereof (a phosphorylating reagent or compound A) to react with a fiber raw material comprising cellulose. It is to be noted that this reaction is performed in the presence of at least one selected from urea and a derivative thereof (hereinafter, referred to as "compound B").
  • One example of the method of allowing compound A to act on the fiber raw material in the presence of compound B may be a method of mixing the fiber raw material that is in a dry or wet state with a powder or a solution of compound A and compound B.
  • Another example thereof may be a method of adding a powder or a solution of compound A and compound B to slurry of the fiber raw material.
  • a method of adding a solution of compound A and compound B to the fiber raw material in a dry state, or a method of adding a powder or a solution of compound A and compound B to the fiber raw material in a wet state is preferable because of the high homogeneity of the reaction.
  • Compound A and compound B may be added at the same time or may be added separately. Alternatively, compound A and compound B to be subjected to the reaction may be first added as a solution, which is then compressed to squeeze out redundant chemicals.
  • the form of the fiber raw material is preferably a cotton-like or thin sheet form, but is not particularly limited thereto.
  • Compound A used in the present embodiment is a compound containing a phosphorus atom and being capable of forming an ester bond with cellulose.
  • Examples of such a compound containing a phosphorus atom and being capable of forming an ester bond with cellulose include at least one selected from phosphoric acid, a salt of phosphoric acid, a dehydrated condensate of phosphoric acid, a salt of dehydrated condensate of phosphoric acid, phosphorus pentoxide and phosphorus oxychloride, or a mixture thereof, but are not particularly limited thereto.
  • Such a compound may contain water in the form of hydrated water or the like, or may also be an anhydride essentially containing no water.
  • a phosphate or a salt of dehydrated condensate of phosphoric acid can be selected from the lithium salt, sodium salt, potassium salt, ammonium salt, organic ammonium salt, and organic phosphonium salt of phosphoric acid or dehydrated condensate of phosphoric acid, and a salt formed with any given compound exhibiting basicity, but examples of such a phosphate or a salt of dehydrated condensate of phosphoric acid are not particularly limited thereto.
  • the degree of neutralization of such a phosphate or a salt of dehydrated condensate of phosphoric acid is not particularly limited, either.
  • phosphoric acid a sodium salt of phosphoric acid, a potassium salt of phosphoric acid, or an ammonium salt of phosphoric acid is preferable.
  • phosphoric acid, ammonium dihydrogen phosphate, or sodium dihydrogen phosphate is more preferable.
  • the compound A is preferably used as a solution.
  • the pH is preferably pH 7 or lower because the efficiency in introduction of phosphoric acid groups becomes high, and more preferably pH 3 or more and 7 or less from the viewpoint of suppression of the hydrolysis of a pulp fiber.
  • the pH of a solution of the compound A may be adjusted, for example, by using, among compounds having phosphoric acid groups, a combination of an acidic one and an alkaline one, and changing the amount ratio thereof.
  • the pH of a solution of compound A may also be adjusted by adding an inorganic alkali or an organic alkali to an acidic compound among compounds having phosphoric acid groups.
  • the amount of the compound A added to a fiber raw material if the amount of the compound A added is converted to a phosphorus atomic weight, the amount of phosphorus atoms added with respect to the fiber raw material (absolute dry mass) is preferably 0.5% by mass or more and 100% by mass or less, more preferably 1% by mass or more and 50% by mass or less, and most preferably 2% by mass or more and 30% by mass or less.
  • the amount of phosphorus atoms added to the fiber raw material is within the above-described range, the yield of ultrafine fibrous cellulose may be further improved.
  • the cost of the compound A used can be reduced by setting the amount of phosphorus atoms added to the fiber raw material at the above-described upper limit value or less.
  • the yield can be increased.
  • Examples of the compound B used in the present embodiment include urea, biuret, 1-phenyl urea, 1-benzyl urea, 1-methyl urea, and 1-ethyl urea.
  • Compound B as with the compound A, is preferably used as a solution.
  • a solution containing both the compound A and the compound B dissolved therein is preferably used because of the enhanced homogeneity of the reaction.
  • the amount of the compound B added to the fiber raw material is preferably 1% by mass or more and 500% by mass or less, more preferably 10% by mass or more and 400% by mass or less, further preferably 100% by mass or more and 350% by mass or less, and particularly preferably 150% by mass or more and 300% by mass or less.
  • the reaction system may comprise an amide or an amine in addition to the compound A and the compound B.
  • the amide include formamide, dimethylformamide, acetamide, and dimethylacetamide.
  • the amine include methylamine, ethylamine, trimethylamine, triethylamine, monoethanolamine, diethanolamine, triethanolamine, pyridine, ethylenediamine, and hexamethylenediamine. Among them, particularly, triethylamine is known to work as a favorable reaction catalyst.
  • a heat treatment is performed.
  • the temperature of the heat treatment it is preferable to select a temperature that allows an efficient introduction of phosphoric acid groups, while suppressing thermal decomposition or hydrolysis reaction of fibers.
  • the temperature 100°C or higher and 300°C or lower, and Further preferably 130°C or higher and 200°C or lower.
  • a vacuum dryer, an infrared heating device, or a microwave heating device may be used for heating.
  • the fiber raw material in the shape of a very thin sheet may be used, or a method of heat-drying or vacuum-drying the fiber raw material, while kneading or stirring with the compound A using a kneader or the like, may be employed.
  • a heating device used for heat treatment a device capable of always discharging moisture retained by slurry or moisture generated by an addition reaction of phosphoric acid groups with hydroxy groups of the fiber to the outside of the device system is preferable, and for example, forced convection ovens or the like are preferable.
  • forced convection ovens or the like are preferable.
  • the time for heat treatment is, although it also depends on the heating temperature, preferably 1 second or more and 300 minutes or less, more preferably 1 second or more and 1000 seconds or less, and further preferably 10 seconds or more and 800 seconds or less, after moisture is substantially removed from the fiber raw material slurry.
  • the heating temperature and heating time within an appropriate range, the amount of phosphoric acid groups introduced can be set within a preferred range.
  • the aforementioned phosphoric acid group introduction step may be carried out at least once, but may also be repeatedly carried out multiple times. For example, it is possible to establish the phosphoric acid group introduction step two times or more and four times or less. However, in the method for producing ultrafine fibrous cellulose of the present invention, even in a case where the aforementioned phosphoric acid group introduction step is carried out only once or twice, the amount of phosphoric acid groups introduced can be sufficiently increased, and the formation of crosslinked structures via phosphoric acid groups can be suppressed.
  • the phosphoric acid group introduction step can be carried out at a small number of times such as once or twice, and thus, an efficient production process can be realized. From the viewpoint of carrying out a more efficient production process, it is preferable to establish the phosphoric acid group introduction step only once.
  • a washing step or an alkaline treatment step may be established between individual phosphoric acid group introduction steps.
  • the after-mentioned step (a2) is preferably carried out, following the final phosphoric acid group introduction step (a1).
  • a step (a2) of forming crosslinked structures via phosphoric acid groups to obtain crosslinked phosphorylated cellulose fibers is established. It is to be noted that the step (a2) may also be incorporated into the heat treatment step in the step (a1).
  • the step (a2) is a heat treatment step.
  • the heating temperature applied in such a heat treatment step is 100°C or higher and 300°C or lower, and preferably 130°C or higher and 200°C or lower.
  • the heating time applied in the heat treatment step is preferably 1 second or more and 300 minutes or less, more preferably 1 second or more and 1000 seconds or less, and further preferably 10 seconds or more and 800 seconds or less.
  • the heat treatment step it is preferable to use, for example, a vacuum dryer, an infrared heating device, or a microwave heating device.
  • the heat treatment step as a step (a2) is preferably carried out continuously after the heat treatment in the aforementioned step (a1) that is a phosphoric acid group introduction step. Thereby, energy efficiency can be enhanced in the step of producing ultrafine fibrous cellulose.
  • the heat treatment step (a2) is carried out continuously after the heat treatment in the step (a1), for example, the heating time can be prolonged while the heat treatment temperature applied in the step (a1) is kept as is. Moreover, by prolonging the heat treatment time in the step (a1), the step (a2) can be substantially incorporated into the step (a1).
  • the heating temperatures applied in the two steps may be set at different temperatures from each other.
  • the amount of phosphoric acid groups contained in the crosslinked phosphorylated cellulose fibers obtained via the step (a1) of introducing phosphoric acid groups and the step (a2) of obtaining crosslinked phosphorylated cellulose fibers is preferably 0.5 mmol/g or more, more preferably 1.0 mmol/g or more, and further preferably 1.6 mmol/g or more.
  • the amount of phosphoric acid groups in ultrafine fibrous cellulose is preferably 5.0 mmol/g or less.
  • the amount of phosphoric acid groups introduced can be measured by a conductometric titration method. Specifically, the amount introduced can be measured by treating the obtained cellulose-containing slurry with an ion exchange resin, and then examining a change in the electrical conductivity while adding a sodium hydroxide aqueous solution.
  • the conductometric titration confers a curve shown in Figure 1 as an alkali is added.
  • first region the electrical conductivity is rapidly reduced
  • second region the conductivity starts rising slightly
  • increment of the conductivity is increased
  • this region is referred to as a "third region”
  • three regions appear.
  • the boundary point between the second region and the third region is defined as a point at which the secondary differential value of conductivity, that is, the change in the increment (gradient) of conductivity becomes maximum.
  • the amount of the alkali required for the first region among these regions is equal to the amount of a strongly acidic group in the slurry used in the titration
  • the amount of the alkali required for the second region is equal to the amount of a weakly acidic group in the slurry used in the titration.
  • the simple term "the amount of the phosphoric acid group introduced (or the amount of the phosphoric acid group)" or "the amount of the substituent introduced (or the amount of the substituent)” refers to the amount of the strongly acidic group. That is to say, the amount (mmol) of the alkali required for the first region in the curve shown in Figure 1 is divided by the solid content (g) in the slurry as a titration target to obtain the amount (mmol/g) of the phosphoric acid group introduced.
  • crosslinked phosphorylated cellulose fibers are obtained.
  • crosslinked structures are formed in an amount of 0.05 mmol/g or more and 2.0 mmol/g or less.
  • the amount of such crosslinked structures is preferably 0.10 mmol/g or more and 1.5 mmol/g or less, and more preferably 0.13 mmol/g or more and 1.0 mmol/g or less.
  • the crosslinked structures are formed as a result of dehydration condensation performed by phosphoric acid groups that have been introduced into cellulose fibers. That is, it is a structure in which a glucose unit of cellulose binds to each of two P atoms of pyrophosphoric acid via an O atom. Accordingly, if crosslinked phosphoric acid groups are formed, weakly acidic groups are apparently lost, and as a result, the amount of alkali necessary for the second region is reduced in comparison to the amount of alkali necessary for the first region in Figure 1 . That is, the amount of the crosslinked structures is a value obtained by dividing a difference between the amount of alkali necessary for the first region and the amount of alkali necessary for the second region by 2.
  • the step (B) is a step of breaking some or all of the crosslinked structures to obtain crosslink-broken phosphorylated cellulose fibers.
  • hydrolysis is carried out to break some or all of the crosslinked structures formed in the step (A).
  • the crosslinked structures are hydrolyzed in an aqueous solvent with pH 3 or more.
  • the above-described aqueous solvent is a solvent comprising at least water, and a pH adjuster and the like. This aqueous solvent is added to the crosslinked phosphorylated cellulose fibers obtained in the step (A), so as to carry out hydrolysis.
  • the pH of a mixture of an aqueous solvent and crosslinked phosphorylated cellulose fibers, which are to be subjected to hydrolysis may be 3 or more, preferably 4 or more, more preferably 6 or more, and further preferably 7 or more.
  • the solvent mixture is preferably an alkaline mixture, and it is preferably a solvent mixture having pH of more than 7.
  • the pH of the solvent mixture is further preferably 8 or more, and particularly preferably 9 or more.
  • the upper limit of the pH of the solvent mixture is not particularly limited, and it may be pH 14.
  • a pH adjuster such as hydrochloric acid or sodium hydroxide is added to water to have a desired pH value.
  • the solvent mixture Upon performing hydrolysis in the step (B), the solvent mixture is heated.
  • the temperature of a mixture of an aqueous solvent and crosslinked phosphorylated cellulose fibers (a solvent mixture) placed in a reaction vessel to be subjected to hydrolysis (hereinafter also referred to as a "internal temperature”) is 80°C or higher.
  • the step (B) in the present invention is preferably a hot alkaline treatment step.
  • the "hot alkaline treatment step” is a treatment step of heating an aqueous solvent with a pH value of more than 7 to 80°C or higher.
  • step (B) preferably 50 mol % or more of, more preferably 55 mol % or more of, and further preferably 60 mol % or more of the crosslinked structures are broken.
  • step (B) 99 mol % or less of the crosslinked structures are preferably broken, based on the total number thereof.
  • the amount of the crosslinked structures in the crosslink-broken phosphorylated cellulose fibers obtained in the step (B) is preferably 0.10 mmol/g or less, and more preferably 0.05 mmol/g or less.
  • the amount of the crosslinked structures in the crosslink-broken phosphorylated cellulose fibers may be 0 mmol/g or more, or may also be 0.003 mmol/g or more.
  • the crosslinked phosphorylated cellulose fibers obtained in the step (A) are converted to crosslink-broken phosphorylated cellulose fibers by being subjected to the aforementioned hydrolysis treatment step.
  • the present invention is also characterized in that the polymerization degree of the crosslink-broken phosphorylated cellulose fibers can be controlled to be within a predetermined range by performing the step (B) under the above-described conditions. That is to say, in the crosslink-broken phosphorylated cellulose fibers obtained in the step (B) of the present invention, it is preferable that the crosslink be broken but the polymerization degree be maintained within a predetermined range.
  • the polymerization degree (DPb) of the crosslink-broken phosphorylated cellulose fibers is preferably 600 or more, more preferably 650 or more, and further preferably 700 or more.
  • the polymerization degree (DPb) of the crosslink-broken phosphorylated cellulose fibers is preferably 1500 or less, and more preferably 880 or less.
  • the value of DPb/DPa is preferably 0.65 or more, more preferably 0.70 or more, and further preferably 0.75 or more.
  • the DPb/DPa value is preferably 1.5 or less, and more preferably 0.94 or less.
  • c indicates the concentration of cellulose fibers at the time of measuring the viscosity.
  • this polymerization degree is an average polymerization degree measured according to viscometry, it is also referred to as a "viscosity average polymerization degree.”
  • Step (C) is a step of performing a mechanical treatment on the crosslink-broken phosphorylated cellulose fibers to obtain fibrous cellulose having a fiber width of 1000 nm or less.
  • a mechanical treatment step is also referred to as a defibration treatment step.
  • the crosslinked structures are broken in the aforementioned step (B)
  • only small energy is needed for the defibration treatment in the step (C)
  • the production cost can be reduced.
  • fibers are defibrated usually using a defibration treatment apparatus to obtain slurry containing ultrafine fibrous cellulose, and there is no particular restriction on a treatment apparatus, or a treatment method.
  • Examples of the defibration treatment apparatus that can be used herein include a high-speed defibrator, a grinder (stone mill-type crusher), a high-pressure homogenizer, an ultrahigh-pressure homogenizer, a high-pressure collision-type crusher, a ball mill, and a bead mill.
  • a wet milling apparatus such as a disc-type refiner, a conical refiner, a twin-screw kneader, an oscillation mill, a homomixer under high-speed rotation, an ultrasonic disperser, or a beater may also be used as such a defibration treatment apparatus.
  • the defibration treatment apparatus is not limited to the above.
  • Examples of a preferred defibration treatment method include a high-speed defibrator, a high-pressure homogenizer, and an ultrahigh-pressure homogenizer, which are less affected by milling media, and are free from apprehension of contamination.
  • the crosslink-broken phosphorylated cellulose fibers obtained in the step (B) are preferably diluted with water and an organic solvent each alone or in combination, to prepare slurry, but the method is not particularly limited thereto.
  • Water as well as a polar organic solvent can be used as a dispersion medium.
  • Preferred examples of the polar organic solvent include, but are not particularly limited to, alcohols, ketones, ethers, dimethyl sulfoxide (DMSO), dimethylformamide (DMF), and dimethylacetamide (DMAc).
  • the alcohols include methanol, ethanol, n-propanol, isopropanol, n-butanol, and t-butyl alcohol.
  • ketones include acetone and methyl ethyl ketone (MEK).
  • ethers include diethyl ether and tetrahydrofuran (THF).
  • One of these dispersion media may be used, or two or more thereof may be used.
  • the dispersion medium may also contain a solid content other than the fiber raw material, for example, hydrogen-binding urea.
  • slurry containing such ultrafine fibrous cellulose may be once concentrated and/or dried, and may be then subjected to a mechanical treatment again.
  • a method in which a concentrating agent is added into slurry containing ultrafine fibrous cellulose and a method using a dehydrator, a press, a dryer, and the like used generally.
  • publicly known methods for example as described in WO 2014/024876 , WO 2012/107642 , and WO 2013/121086 , may be used.
  • the ultrafine fibrous cellulose-containing slurry is concentrated and dried by forming a sheet from the slurry, and a mechanical treatment is then carried out on the sheet, so that the ultrafine fibrous cellulose-containing slurry can be obtained again.
  • a high-speed defibrator As an apparatus used for defibrating (pulverizing) again the ultrafine fibrous cellulose-containing slurry after it has been concentrated and/or dried, a high-speed defibrator, a grinder (stone mill-type grinder), a high-pressure homogenizer, an ultra-high pressure homogenizer, a high-pressure collision type crusher, a ball mill, a bead mill, a disk type refiner, a conical refiner, a twin screw kneader, a vibrating mill, a device for wet milling, such as a high-speed rotating homomixer, an ultrasonic disperser, and a beater may be used, but examples of the apparatus are not particularly limited thereto.
  • ultrafine fibrous cellulose having phosphoric acid groups is obtained.
  • the ultrafine fibrous cellulose is preferably obtained in the form of slurry, but it may also be obtained as a particulate.
  • a concentration step, a drying step and the like may be established, as appropriate.
  • the polymerization degree of the fibrous cellulose having a fiber width of 1000 nm or less (ultrafine fibrous cellulose) obtained in the step (C) is preferably 390 or more, and more preferably 400 or more.
  • the polymerization degree of the fibrous cellulose is preferably 1000 or less, and more preferably 450 or less.
  • the above-described polymerization degree of the ultrafine fibrous cellulose can be calculated by the same method as the aforementioned method of measuring the polymerization degree of the cellulose fibers obtained in the step (B).
  • the aforementioned phosphoric acid group introduction step (a1) in the step (A) is preferably carried out only once, but the step (a1) may also be repeated multiple times.
  • a washing step or an alkaline treatment step may be established between individual phosphoric acid group introduction steps.
  • such a washing step or an alkaline treatment step may also be established between the aforementioned step (A) and step (B).
  • the washing step can be carried out by repeatedly performing an operation of pouring ion exchange water onto the cellulose fibers obtained in the step before the washing step, then stirring the solution to uniformly disperse the cellulose fibers therein, and then performing filtration and dehydration to obtain a dehydrated sheet.
  • the washing step can be carried out by repeatedly performing an operation of pouring ion exchange water onto the cellulose fibers obtained in the step before the washing step, then stirring the solution to uniformly disperse the cellulose fibers therein, and then performing filtration and dehydration to obtain a dehydrated sheet.
  • the alkaline treatment method in the alkaline treatment step is not particularly limited.
  • a method of immersing cellulose fibers in an alkaline solution may be applied.
  • the alkaline compound contained in the alkaline solution is not particularly limited, and it may be either an inorganic alkaline compound or an organic alkaline compound.
  • the solvent in the alkaline solution may be either water or an organic solvent.
  • the solvent is preferably a polar solvent (water, or a polar organic solvent such as alcohol), and more preferably an aqueous solvent containing at least water.
  • a sodium hydroxide aqueous solution, or a potassium hydroxide aqueous solution is particularly preferable because of their multiplicity of uses.
  • the temperature of the alkaline solution in the alkaline treatment step is not particularly limited, and it is preferably 5°C or higher and 80°C or lower, and more preferably 10°C or higher and 60°C or lower.
  • the time required for immersion of cellulose fibers in the alkaline solution in the alkaline treatment step is not particularly limited, and it is preferably 5 minutes or more and 30 minutes or less, and more preferably 10 minutes or more and 20 minutes or less.
  • the amount of the alkaline solution used in the alkaline treatment is not particularly limited, and it is preferably 100% by mass or more and 100000% by mass or less, and more preferably 1000% by mass or more and 10000% by mass or less, based on the absolute dry mass of the cellulose fibers.
  • a washing step as described above may be preferably established before the alkaline treatment step.
  • the alkali-treated cellulose fibers are preferably washed with water or an organic solvent, in order to improve handling ability.
  • the present invention relates to fibrous cellulose with a fiber width of 1000 nm or less (also referred to as "ultrafine fibrous cellulose") having phosphoric acid groups, which is produced by the aforementioned production method.
  • the amount of phosphoric acid groups contained in the ultrafine fibrous cellulose of the present invention is preferably 1.65 mmol/g or more, and the polymerization degree of the ultrafine fibrous cellulose is preferably 390 or more.
  • the formation of crosslinked structures via phosphoric acid groups is reduced, but at least some crosslinked structures remain in the ultrafine fibrous cellulose.
  • the ultrafine fibrous cellulose of the present invention comprises crosslinked structures formed via phosphoric acid groups.
  • the present invention has been made to solve the aforementioned problems, and even if the amount of phosphoric acid introduced is large, the polymerization degree of phosphorylated ultrafine fibrous cellulose can be kept at a predetermined value or more. Furthermore, in the ultrafine fibrous cellulose of the present invention, even if the amount of phosphoric acid introduced is large, the number of crosslinked structures is controlled to be small. Fibrillation is favorably done in such ultrafine fibrous cellulose, and when the ultrafine fibrous cellulose is processed into, for example, slurry, the slurry can exhibit high viscosity.
  • the fibrous cellulose raw material for obtaining ultrafine fibrous cellulose is not particularly limited. From the viewpoint of availability and inexpensiveness, pulp is preferably used.
  • the pulp include wood pulp, non-wood pulp, and deinked pulp.
  • the wood pulp include chemical pulps such as leaf bleached kraft pulp (LBKP), needle bleached kraft pulp (NBKP), sulfite pulp (SP), dissolving pulp (DP), soda pulp (AP), unbleached kraft pulp (UKP), and oxygen bleached kraft pulp (OKP).
  • semichemical pulps such as semi-chemical pulp (SCP) and chemi-ground wood pulp (CGP); and mechanical pulps such as ground pulp (GP) and thermomechanical pulp (TMP, BCTMP).
  • non-wood pulp include, but are not particularly limited to, cotton pulps such as cotton linter and cotton lint; non-wood type pulps such as hemp, wheat straw, and bagasse; and cellulose isolated from ascidian, seaweed, etc., chitin, and chitosan.
  • deinked pulp there is deinked pulp using waste paper as a raw material, but it is not particularly limited thereto.
  • the pulp of the present embodiment may be used singly, or in combination of two or more types.
  • wood pulp and deinked pulp including cellulose are preferable from the viewpoint of easy availability.
  • chemical pulp is preferable because it has a higher cellulose content to enhance the yield of ultrafine fibrous cellulose and decomposition of cellulose in the pulp is mild at the time of ultrafine fiber formation (defibration) to yield ultrafine fibrous cellulose having a long fiber length with a high aspect ratio.
  • kraft pulp and sulfite pulp are most preferably selected.
  • the average fiber width of the ultrafine fibrous cellulose is 1000 nm or less according to observation with an electron microscope.
  • the average fiber width is preferably 2 nm or more and 1000 nm or less, more preferably 2 nm or more and 100 nm or less, even more preferably 2 nm or more and 50 nm or less, and further preferably 2 nm or more and 10 nm or less, but is not particularly limited thereto.
  • the ultrafine fibrous cellulose is, for example, monofilament cellulose having a fiber width of 1000 nm or less.
  • the measurement of a fiber width of ultrafine fibrous cellulose by electron microscopic observation is carried out as follows.
  • An aqueous suspension of ultrafine fibrous cellulose having a concentration of 0.05% by mass or more and 0.1% by mass or less is prepared, and the suspension is casted onto a hydrophilized carbon film-coated grid as a sample for TEM observation. If the sample contains wide fibers, SEM images of the surface of the suspension casted onto glass may be observed.
  • the sample is observed using electron microscope images taken at a magnification of 1000x, 5000x, 10000 ⁇ , or 50000x according to the widths of the constituent fibers. However, the sample, the observation conditions, and the magnification are adjusted so as to satisfy the following conditions:
  • the average fiber width (which is simply referred to as a "fiber width" at times) of ultrafine fibrous cellulose is an average value of the fiber widths thus read.
  • the fiber length of the ultrafine fibrous cellulose is not particularly limited, and it is preferably 0.1 ⁇ m or more and 1000 ⁇ m or less, more preferably 0.1 ⁇ m or more and 800 ⁇ m or less, and particularly preferably 0.1 ⁇ m or more and 600 ⁇ m or less.
  • the fiber length of the ultrafine fibrous cellulose can be obtained by an image analysis using TEM, SEM or AFM.
  • Ultrafine fibrous cellulose preferably has a type I crystal structure.
  • the percentage (crystallinity) of the type I crystal structure occupied in the ultrafine fibrous cellulose is not particularly limited in the present invention, and for example, it is preferably 30% or more, more preferably 50% or more, and further preferably 70% or more. In this case, more excellent performance can be expected, in terms of heat resistance and the expression of low linear thermal expansion.
  • the crystallinity can be obtained by measuring an X-ray diffraction profile and obtaining it according to a common method ( Seagal et al., Textile Research Journal, Vol. 29, p. 786, 1959 ).
  • the ultrafine fibrous cellulose of the present invention has phosphoric acid groups.
  • the "phosphoric acid group” includes a phosphoric acid group and a substituent derived from such a phosphoric acid group.
  • the phosphoric acid group is a divalent functional group corresponding to phosphoric acid from which a hydroxyl group is removed. Specifically, it is a group represented by -PO 3 H 2 .
  • the substituents derived from the phosphoric acid group include substituents, such as condensation-polymerized phosphoric acid groups, salts of phosphoric acid groups, and phosphoric acid ester groups, and they may be either ionic substituents or nonionic substituents.
  • the phosphoric acid group or a substituent derived from the phosphoric acid group may be a substituent represented by the following structural formula:
  • R is a hydrogen atom, a saturated straight chain hydrocarbon group, a saturated branched chain hydrocarbon group, a saturated cyclic hydrocarbon group, an unsaturated straight chain hydrocarbon group, an unsaturated branched chain hydrocarbon group, an aromatic group, or a derivative group thereof.
  • ⁇ is a monovalent or higher valent cation consisting of organic matter or inorganic matter.
  • the amount of phosphoric acid groups in the ultrafine fibrous cellulose is preferably 1.00 mmol/g or more, more preferably 1.20 mmol/g or more, further preferably 1.65 mmol/g or more, and particularly preferably 1.80 mmol/g or more.
  • the amount of phosphoric acid groups in the ultrafine fibrous cellulose is preferably 5.0 mmol/g or less.
  • the amount of phosphoric acid groups introduced may be measured by the aforementioned conductometric titration method. Specifically, the amount introduced may be measured by performing fibrillation on ultrafine fibers in the mechanical treatment step, treating the obtained ultrafine fibrous cellulose-containing slurry with an ion exchange resin, and then examining a change in the electrical conductivity while adding an aqueous sodium hydroxide solution.
  • the polymerization degree of the ultrafine fibrous cellulose is preferably 390 or more, and more preferably 400 or more.
  • the polymerization degree of the ultrafine fibrous cellulose is preferably 1000 or less, and more preferably 450 or less.
  • the above-described polymerization degree of the ultrafine fibrous cellulose can be calculated by the same method as the aforementioned method of measuring the polymerization degree of the ultrafine fibrous cellulose obtained in the step (B).
  • step (A) when phosphoric acid groups are introduced into cellulose fibers to obtain phosphorylated cellulose fibers, urea and/or a derivative thereof being used as a phosphorylating agent, as well as a compound having a phosphoric acid group, groups having a urethane bond is introduced as a group derived from such urea and/or a derivative thereof into cellulose.
  • the content of the groups having a urethane bond is preferably 0.3 mmol/g or less, more preferably 0.2 mmol/g or less, and further preferably 0.1 mmol/g or less, with respect to 1 g of the ultrafine fibrous cellulose.
  • the content of the groups having a urethane bond may also be 0 mmol/g.
  • an example of the group having a urethane bond may be a group represented by the following structural formula:
  • R represents a hydrogen atom, a saturated straight chain hydrocarbon group, a saturated branched chain hydrocarbon group, a saturated cyclic hydrocarbon group, an unsaturated straight chain hydrocarbon group, an unsaturated branched chain hydrocarbon group, an aromatic group, or a derivative group thereof
  • the amount of the groups having a urethane bond introduced can be determined by measuring the amount of nitrogen covalently bound to cellulose. Specifically, after ionic nitrogen (ammonium ions) has been released and removed, the amount of nitrogen is measured according to a trace nitrogen analysis method. The release of ionic nitrogen (ammonium ions) is carried out under conditions where nitrogen covalently bound to cellulose is not substantially removed. The removal of the released ammonium ions is carried out by the same method as the measurement of the amount of phosphoric acid groups introduced. Specifically, the removal is carried out by adsorbing ammonium ions on a strongly acidic ion exchange resin.
  • the measurement is carried out using the trace total nitrogen analyzer TN-110, manufactured by Mitsubishi Chemical Analytech Co., Ltd. Before performing the measurement, a solvent is removed by drying a sample at a low temperature (for example, at 40°C for 24 hours in a vacuum dryer).
  • the present invention also relates to slurry containing fibrous cellulose with a fiber width of 1000 nm or less having phosphoric acid groups (hereinafter also referred to as "ultrafine fibrous cellulose-containing slurry).
  • the viscosity at 25°C of the ultrafine fibrous cellulose-containing slurry of the present invention is preferably 9500 mPa ⁇ s or more.
  • the viscosity of the ultrafine fibrous cellulose-containing slurry is the viscosity of slurry that is dispersed in ion exchange water so that the concentration of the ultrafine fibrous cellulose can be 0.4% by mass.
  • the viscosity of the slurry is preferably 9500 mPa ⁇ s or more, more preferably 10000 mPa ⁇ s or more, and more preferably 12000 mPa ⁇ s or more.
  • the upper limit value of the viscosity of the slurry is not particularly limited, and it can be, for example, 40000 mPa ⁇ s.
  • the viscosity of the ultrafine fibrous cellulose-containing slurry (concentration of the ultrafine fibrous cellulose: 0.4% by mass) can be measured using a type B viscometer (analog viscometer T-LVT, manufactured by BROOKFIELD). The viscosity is measured by rotating the dispersed solution under measurement conditions of 25°C at a rotation number of 3 rpm for 3 minutes.
  • the haze of the ultrafine fibrous cellulose-containing slurry (concentration of the ultrafine fibrous cellulose: 0.2% by mass) is preferably 20% or less, more preferably 15% or less, and further preferably 10% or less.
  • the haze of the ultrafine fibrous cellulose-containing slurry which is within the above-described range, means that the ultrafine fibrous cellulose-containing slurry has high transparency and favorable fibrillation of the ultrafine fibrous cellulose. In such ultrafine fibrous cellulose-containing slurry, specific functions possessed by the ultrafine fibrous cellulose are exhibited.
  • the haze of the ultrafine fibrous cellulose-containing slurry is a value measured by placing the ultrafine fibrous cellulose-containing slurry into a glass cell for liquid having an optical path length of 1 cm (MG-40, manufactured by Fujiwara Scientific Company Co., Ltd., inverse optical path), and then measuring the haze thereof using a haze meter (HM-150, manufactured by MURAKAMI COLOR RESEARCH LABORATORY Co., Ltd.) in accordance with JIS K 7136. It is to be noted that the measurement of zero point is carried out with ion exchange water filled in the same glass cell as that described above.
  • the yield of a supernatant obtained after the centrifugation of the ultrafine fibrous cellulose-containing slurry is preferably 50% or more, more preferably 70% or more, and further preferably 75% or more.
  • the supernatant yield obtained after the centrifugation is used as an indicator of the yield of the ultrafine fibrous cellulose. The higher the supernatant yield, the higher the yield of the ultrafine fibrous cellulose that can be obtained.
  • Ion exchange water is added to the ultrafine fibrous cellulose-containing slurry, and the concentration of a solid thereof is then adjusted to 0.2% by mass to obtain slurry (defined as slurry A).
  • slurry A a cooled high-speed centrifuge (H-2000B, KOKUSAN Co., Ltd.)
  • H-2000B cooled high-speed centrifuge
  • the slurry A is centrifuged under conditions of 12000 G for 10 minutes.
  • the obtained supernatant (defined as slurry B) is recovered, and the concentration of a solid in the supernatant is then measured.
  • a supernatant yield (the yield of the ultrafine fibrous cellulose) is obtained.
  • Supernatant yield % solid concentration % by mass of slurry B / solid concentration % by mass of slurry A ⁇ 100
  • the present invention relates to a sheet comprising fibrous cellulose with a fiber width of 1000 nm or less having phosphoric acid groups (hereinafter also referred to as an "ultrafine fibrous cellulose-containing sheet").
  • a sheet comprising fibrous cellulose with a fiber width of 1000 nm or less having phosphoric acid groups (hereinafter also referred to as an "ultrafine fibrous cellulose-containing sheet").
  • the ultrafine fibrous cellulose-containing sheet of the present invention when the YI value obtained after performing vacuum drying on a sheet at 200°C for 4 hours is defined as YI 2 , and the YI value obtained before performing vacuum drying on a sheet at 200°C for 4 hours is defined as YI 1 , the ⁇ YI value represented by YI 2 -YI 1 is preferably 20 or less.
  • the ⁇ YI value indicates a change in yellowness before and after a heat treatment at 200°C, and the ⁇ YI value is more preferably 15 or less, and further preferably 10 or less. According to the present invention, the ⁇ YI value of the ultrafine fibrous cellulose-containing sheet can be reduced.
  • the YI value is an indicator that indicates the yellowness of a sheet.
  • YI value is a value measured in accordance with JIS K 7373, using Colour Cute i (manufactured by Suga Test Instruments Co., Ltd.).
  • a factor for suppressing a yellowness change in the ultrafine fibrous cellulose-containing sheet of the present invention is unknown. It is considered that suppression of such a yellowness change would be caused by a reduction in the amount of groups having a urethane bond contained in the ultrafine fibrous cellulose. That is to say, if groups having a urethane bond remain, nitrogen glycosides are generated as a result of thermal decomposition, and subsequently, an aminocarbonyl reaction, and then, a dehydration reaction from chain saccharides, etc. take place, and generation of coloring components is likely to increase. In the present invention, since the amount of groups having a urethane bond contained in the ultrafine fibrous cellulose is small, a yellowness change is considered to be suppressed.
  • the tensile strength of the ultrafine fibrous cellulose-containing sheet of the present invention is preferably 80 MPa or more, more preferably 90 MPa or more, and further preferably 100 MPa or more.
  • the tensile strength of the ultrafine fibrous cellulose-containing sheet of the present invention is a value measured by using a test piece that has been subjected to humidity control at a temperature of 23°C and at a relative humidity of 50% for 24 hours, and employing the tension testing machine Tensilon (manufactured by A & D Company, Limited), in accordance with JIS K 8113.
  • the basis weight of the ultrafine fibrous cellulose-containing sheet of the present invention is preferably 10 g/m 2 or more, more preferably 20 g/m 2 or more, and further preferably 30 g/m 2 or more.
  • the density of the ultrafine fibrous cellulose-containing sheet is preferably 60 g/m 2 or less.
  • the basis weight of the sheet can be calculated in accordance with JIS P 8124.
  • the thickness of the ultrafine fibrous cellulose-containing sheet of the present invention is not particularly limited. It is preferably 5 ⁇ m or more, more preferably 10 ⁇ m or more, and further preferably 20 ⁇ m or more.
  • the upper limit value of the sheet is not particularly limited, and it may be set, for example, at 1000 ⁇ m or less.
  • the step of producing a sheet includes a step of obtaining slurry containing fibrous cellulose having a fiber width of 1000 nm or less, a step of applying this slurry onto a base material, or a step of making a paper from the slurry.
  • the step of producing a sheet preferably includes a step of applying slurry containing ultrafine fibrous cellulose (hereinafter also referred to simply as "slurry") onto a base material.
  • optional components such as antifoaming agents, lubricants, ultraviolet absorbing agents, dyes, pigments, stabilizers, and surfactants may be added into slurry.
  • optional components include hydrophilic polymers and organic ions.
  • the hydrophilic polymers are preferably hydrophilic oxygen-containing organic compounds (except for the above-described cellulose fibers).
  • Oxygen-containing organic compounds may be added, as appropriate.
  • the oxygen-containing organic compounds include: hydrophilic polymers, such as polyethylene glycol, polyethylene oxide, casein, dextrin, starches, modified starches, polyvinyl alcohol, modified polyvinyl alcohol (such as acetoacetylated polyvinyl alcohol), polyethylene oxide, polyvinyl pyrrolidone, polyvinyl methyl ether, polyacrylates, alkyl acrylate ester copolymers, urethane-based copolymers, and cellulose derivatives (such as hydroxyethyl cellulose, carboxyethyl cellulose, and carboxymethyl cellulose); and hydrophilic small molecules, such as glycerin, sorbitol, and ethylene glycol.
  • hydrophilic polymers such as polyethylene glycol, polyethylene oxide, casein, dextrin, starches, modified starches, polyvinyl alcohol, modified polyvinyl alcohol (such as acetoacetylated poly
  • oxygen-containing organic compounds are preferably polyethylene glycol, polyethylene oxide, glycerin and sorbitol, and more preferably at least one selected from polyethylene glycol and polyethylene oxide.
  • Examples of the organic ions include tetraalkylammonium ions and tetraalkylphosphonium ions.
  • Examples of the tetraalkylammonium ions include a tetramethylammonium ion, a tetraethylammonium ion, a tetrapropylammonium ion, a tetrabutylammonium ion, a tetrapentylammonium ion, a tetrahexylammonium ion, a tetraheptylammonium ion, a tributylmethylammonium ion, a lauryltrimethylammonium ion, a cetyltrimethylammonium ion, a stearyltrimethylammonium ion, an octyldimethylethylammonium ion, a lauryldimethylethy
  • tetraalkylphosphonium ions examples include a tetramethylphosphonium ion, a tetraethylphosphonium ion, a tetrapropylphosphonium ion, a tetrabutylphosphonium ion, and a lauryltrimethylphosphonium ion.
  • tetrapropylonium ions and tetrabutylonium ions may include tetra-n-propylonium ions and tetra-n-butylonium ions, respectively.
  • the coating step is a step of applying slurry onto a base material, drying the slurry to form a sheet, and detaching the sheet from the base material to obtain a sheet.
  • Use of a coating apparatus and a long base material can continuously produce sheets.
  • the quality of the base material used in the coating step is not particularly limited. Although a base material having higher wettability to the slurry is preferable because shrinkage of the sheet or the like upon drying is suppressed, it is preferable to select one from which a sheet formed after drying can be easily detached. Of these, a resin plate or a metal plate is preferable, without particular limitation.
  • the base material that can be used herein include resin plates such as acrylic plates, polyethylene terephthalate plates, vinyl chloride plates, polystyrene plates, and polyvinylidene chloride plates; metal plates such as aluminum plates, zinc plates, copper plates, and iron plates; plates obtained by the oxidation treatment of the surface thereof; and stainless steel plates and brass plates.
  • a damming frame may be fixed and used on the base material in order to obtain a sheet having a predetermined thickness and basis weight.
  • the quality of the damming frame is not particularly limited, and it is preferable to select ones from which the edges of the sheet adhering after drying can be easily detached.
  • frames formed from resin plates or metal plates are preferable, without particular limitation.
  • Example of the frames that can be used herein include frames formed from resin plates such as acrylic plates, polyethylene terephthalate plates, vinyl chloride plates, polystyrene plates, and polyvinylidene chloride plates; from metal plates such as aluminum plates, zinc plates, copper plates, and iron plates; from plates obtained by the oxidation treatment of surface thereof; and from stainless steel plates and brass plates.
  • resin plates such as acrylic plates, polyethylene terephthalate plates, vinyl chloride plates, polystyrene plates, and polyvinylidene chloride plates
  • metal plates such as aluminum plates, zinc plates, copper plates, and iron plates
  • plates obtained by the oxidation treatment of surface thereof and from stainless steel plates and brass plates.
  • Examples of a coater for applying the slurry that can be used herein include roll coaters, gravure coaters, die coaters, curtain coaters, and air doctor coaters. Die coaters, curtain coaters, and spray coaters are preferable because more even thickness can be provided.
  • the coating temperature is not particularly limited, and it is preferably 20°C or higher and 45°C or lower, more preferably 25°C or higher and 40°C or lower, and further preferably 27°C or higher and 35°C or lower.
  • the coating temperature is equal to or higher than the above-described lower limit value, it is possible to easily apply the slurry.
  • the coating temperature is equal to or lower than the above-described upper limit value, it is possible to prevent volatilization of the dispersion medium upon coating.
  • the coating step it is preferable to apply the slurry so as to achieve a finished basis weight of the sheet of 10 g/m 2 or more and 100 g/m 2 or less, and preferably 20 g/m 2 or more and 60 g/m 2 or less.
  • a sheet having excellent strength can be obtained.
  • the coating step preferably includes a step of drying the slurry applied onto the base material.
  • the drying method is not particularly limited, and any of a contactless drying method and a method of drying the sheet while locking the sheet may be used, or these methods may also be used in combination.
  • the contactless drying method is not particularly limited, and a method for drying by heating with hot air, infrared radiation, far-infrared radiation, or near-infrared radiation (a drying method by heating) or a method for drying in vacuum (a vacuum drying method) can be utilized. Although the drying method by heating and the vacuum drying method may be combined, the drying method by heating is usually utilized.
  • the drying with infrared radiation, far-infrared radiation, or near-infrared radiation can be performed using an infrared apparatus, a far-infrared apparatus, or a near-infrared apparatus without particular limitations.
  • the heating temperature for the drying method by heating is not particularly limited, and it is preferably 20°C or higher and 150°C or lower, and more preferably 25°C or higher and 105°C or lower.
  • the dispersion medium can be rapidly volatilized.
  • cost required for the heating can be reduced, and thermal discoloration of the ultrafine fibrous cellulose can be suppressed.
  • the step of producing the sheet of the present invention may include a step of papermaking from slurry.
  • a paper machine used in the papermaking step include continuous paper machines such as a Fourdrinier paper machine, a cylinder paper machine, and an inclined paper machine, and a multilayer combination paper machine, which is a combination thereof.
  • Known papermaking such as papermaking by hand may be carried out in the papermaking step.
  • filter fabric for filtration is not particularly limited. It is important that ultrafine fibrous cellulose or polyamine polyamide epihalohydrin do not pass through the filter fabric and the filtration speed does not become excessively slow.
  • filter fabric is not particularly limited, and a sheet comprising organic polymers, woven fabric, or porous membrane is preferred.
  • organic polymers include, but are not particularly limited to, non-cellulose organic polymers such as polyethylene terephthalate, polyethylene, polypropylene, and polytetrafluoroethylene (PTFE).
  • a method for producing a sheet from slurry is not particularly limited, and an example thereof is a method of using the production apparatus disclosed in WO 2011/013567 .
  • This production apparatus comprises a dewatering section for ejecting slurry containing ultrafine fibrous cellulose onto the upper surface of an endless belt and then dewatering a dispersion medium contained in the ejected slurry to form a web, and a drying section for drying the web to produce a fiber sheet.
  • the endless belt is provided across from the dewatering section to the drying section, and the web formed in the dewatering section is transferred to the drying section while being placed on the endless belt.
  • An adoptable dehydration method is not particularly limited.
  • An example of the method is a dehydration method conventionally used for paper production.
  • a preferred example is a method comprising performing dehydration using a Fourdrinier, cylinder, tilted wire, or the like and then performing dehydration using a roll press.
  • a drying method is not particularly limited, and an example thereof is a method used for paper production and for example, a method using a cylinder dryer, a yankee dryer, hot air drying, a near-infrared heater, or an infrared heater is preferred.
  • the sheet of the present invention includes a composite sheet comprising a resin component in addition to ultrafine fibrous cellulose.
  • the resin component may be, for example, a natural resin or a synthetic resin.
  • Examples of natural resins may include rosin-based resins, such as rosin, rosin ester and hydrogenated rosin ester.
  • the synthetic resin is preferably at least one selected from, for example, polycarbonate resins, polyethylene terephthalate resins, polyethylene naphthalate resins, polyethylene resins, polypropylene resins, polyimide resins, polystyrene resins and acrylic resins.
  • the synthetic resin is preferably at least one selected from polycarbonate resins and acrylic resins, and more preferably a polycarbonate resin.
  • the acrylic resin is preferably at least any one selected from polyacrylonitrile and poly(meth)acrylate.
  • polycarbonate resin examples include aromatic polycarbonate-based resins and aliphatic polycarbonate-based resins. These specific polycarbonate-based resins are known, and the polycarbonate-based resin described in JP-A-No. 2010-023275 is included, for example.
  • the aforementioned resin component may be present in a composite sheet, in a state in which it is uniformly dispersed, or may also be unevenly distributed in the composite sheet. That is to say, in the step of producing a composite sheet, slurry in which ultrafine fibrous cellulose and a resin component are uniformly mixed with each other may be obtained, and a composite sheet may be then formed from the slurry. Otherwise, a composite sheet having a laminated structure consisting of an ultrafine fibrous cellulose layer and a resin layer may also be formed.
  • ultrafine fibrous cellulose produced by the method for producing fibrous cellulose of the present invention the amount of phosphoric acid groups introduced can be easily controlled, and the fibrillation thereof is favorably achieved.
  • a sheet comprising the ultrafine fibrous cellulose has low yellowness (YI value). Even in the case of drying the sheet by heating it, an increase in the yellowness of the sheet is suppressed.
  • the fibrous cellulose of the present invention is suitable for purposes such as various display devices, light transmissive substrates for various solar cells, and the like.
  • the fibrous cellulose of the present invention is suitable for purposes such as substrates for electronics, members for home electronics, window materials for various vehicles or buildings, interior materials, exterior materials, and packaging materials. Furthermore, the fibrous cellulose of the present invention is also suitable for purposes such as threads, filters, woven fabrics, buffering materials, sponges, polishing materials, and other purposes of using the sheet itself as a reinforcing material.
  • the fibrous cellulose of the present invention can be used as a thickener for various intended uses (for example, as an additive or the like for food products, cosmetic products, cements, paints, inks, etc.).
  • a pulp manufactured by Oji Paper Co., Ltd. (sheet-like pulp having a solid content of 93% and a basis weight of 208 g/m 2 , and a Canadian standard freeness (CSF) measured according to JIS P8121 after disintegration of 700 ml) was used.
  • a mixed aqueous solution of ammonium dihydrogen phosphate and urea was added to 100 parts by weight of the above-described leaf bleached kraft pulp (absolute dry mass), and the resultant mixture was pressed to 48 parts by mass of ammonium dihydrogen phosphate, 130 parts by mass of urea and 165 parts by mass of ion exchange water, so as to obtain a chemical-impregnated pulp.
  • the obtained chemical-impregnated pulp was dried and heat-treated for 200 seconds in a hot air dryer at 165°C to introduce phosphoric acid groups into the cellulose in the pulp, so as to obtain phosphorylated cellulose fibers A.
  • Ion exchange water was poured onto the obtained phosphorylated cellulose fibers A, which was then uniformly dispersed by stirring, filtered, and dehydrated to obtain a dehydrated sheet. This operation was repeated to thoroughly wash off redundant chemicals. Subsequently, the dehydrated sheet was diluted with ion exchange water to cellulose fibers concentration of 2% by mass. A 1 N aqueous solution of sodium hydroxide was gradually added, while stirring, to obtain pulp slurry having pH 12 ⁇ 0.2. Then, this pulp slurry was dehydrated to obtain a dehydrated sheet. Then, ion exchange water was poured again onto the dehydrated sheet, which was then uniformly dispersed by stirring, filtered, and dehydrated to obtain a dehydrated sheet. This operation was repeatedly carried out to thoroughly wash off redundant sodium hydroxide, so as to obtain phosphorylated cellulose fibers B.
  • the aforementioned ⁇ phosphorylation reaction step > was repeatedly carried out, so that phosphoric acid groups were further introduced into the cellulose in the pulp, thereby obtaining phosphorylated cellulose fibers C.
  • the obtained phosphorylated cellulose fibers C was heat-treated for 200 seconds in a hot air dryer at 165°C to further introduce phosphoric acid groups into the cellulose in the pulp.
  • crosslinked structures were also introduced into the cellulose, mediated by the phosphoric acid groups, so as to obtain crosslinked phosphorylated cellulose fibers A.
  • this crosslinking step was carried out, while the drying and/or heating time applied to the phosphoric acid group introduction step (second step) was prolonged (i.e., a heat treatment was carried out in a total of 400 seconds in a hot air dryer at 165°C).
  • the aforementioned ⁇ washing and/or alkaline treatment step > was carried out on the obtained crosslinked phosphorylated cellulose fibers A to obtain crosslinked phosphorylated cellulose fibers B.
  • Ion exchange water and NaOH were added to the obtained crosslinked phosphorylated cellulose fibers B, so that the solid concentration of the crosslinked phosphorylated cellulose fibers B could be 2.0% by mass and the pH value thereof could be pH 12.5, thereby obtaining pulp slurry.
  • the obtained pulp slurry was heated, while it was left at rest, under conditions of an internal temperature of 90°C for 1 hour. Thereafter, this pulp slurry was dehydrated to obtain a dehydrated sheet.
  • Ion exchange water was poured onto the dehydrated sheet again, was then uniformly dispersed by stirring, and was then filtered and dehydrated to obtain a dehydrated sheet. This operation was repeatedly carried out to thoroughly wash off redundant sodium hydroxide, so as to obtain crosslink-broken phosphorylated cellulose fibers A.
  • the polymerization degree of the obtained crosslink-broken phosphorylated cellulose fibers A was measured by the after-mentioned method.
  • Ion exchange water was added to the obtained crosslink-broken phosphorylated cellulose fibers A to prepare a suspension having a solid concentration of 2.0% by mass.
  • This suspension was subjected to a mechanical treatment using a wet-type atomizing device (ALTIMIZER, manufactured by Sugino Machine Ltd.) to obtain ultrafine fibrous cellulose-containing slurry.
  • ATIMIZER a wet-type atomizing device manufactured by Sugino Machine Ltd.
  • ultrafine fibrous cellulose-containing slurry passed through the processing chamber once at a pressure of 200 MPa (for use in the measurement of supernatant yield, haze, viscosity, and urethane bond amount) and ultrafine fibrous cellulose-containing slurry passed through the processing chamber five times at a pressure of 200 MPa (for use in the measurement of phosphoric acid group amount and crosslinked structure amount) were obtained.
  • the obtained ultrafine fibrous cellulose-containing slurry was measured according to the after-mentioned methods, in terms of supernatant yield, haze, viscosity, the amount of urethane bonds, the amount of phosphoric acid groups, and the content of crosslinked structures.
  • Polyethylene glycol (molecular weight: 4,000,000; manufactured by Wako Pure Chemical Industries, Ltd.) was added to the ultrafine fibrous cellulose-containing slurry, such that 20 parts by mass of polyethylene glycol could be added to 100 parts by mass of the ultrafine fibrous cellulose. Moreover, ion exchange water was added to the slurry, such that a total solid concentration of the ultrafine fibrous cellulose and polyethylene glycol could be 0.5% by mass, and the obtained mixture was then stirred so that the solution could be fully uniform and the concentration could be adjusted, thereby obtaining a suspension.
  • the suspension was weighed so that the finished basis weight of the sheet could be 45 g/m 2 , was then developed on a commercially available acrylic plate, and was then dried in a chamber at 35°C and a relative humidity of 15%.
  • a plate for damming was arranged on the acrylic plate so as to have a predetermined basis weight.
  • an ultrafine fibrous cellulose-containing sheet was obtained, and the thickness thereof was 30 ⁇ m.
  • the obtained ultrafine fibrous cellulose-containing sheet was measured according to the after-mentioned methods, in terms of tensile strength and YI values before and after heating.
  • a pulp manufactured by Oji Paper Co., Ltd. (sheet-like pulp having a solid content of 93% and a basis weight of 208 g/m 2 , and a Canadian standard freeness (CSF) measured according to JIS P8121 after disintegration of 700 ml) was used.
  • a mixed aqueous solution of ammonium dihydrogen phosphate and urea was added to 100 parts by weight of the above-described leaf bleached kraft pulp (absolute dry mass), and the resultant mixture was pressed to 56 parts by mass of ammonium dihydrogen phosphate, 150 parts by mass of urea and 165 parts by mass of ion exchange water, so as to obtain a chemical-impregnated pulp.
  • the obtained chemical-impregnated pulp was heated in a hot air dryer at 105°C, so that water was evaporated to carry out pre-drying. Thereafter, the chemical-impregnated pulp was dried and heat-treated for 30 minutes in a hot air dryer at 140°C to introduce phosphoric acid groups into the cellulose in the pulp, so as to obtain phosphorylated cellulose fibers A.
  • crosslinked structures were introduced into cellulose, mediated by the phosphoric acid groups. That is to say, the crosslinking step was carried out at the same time as the phosphorylation reaction step.
  • the ⁇ washing and/or alkaline treatment step >, ⁇ crosslink-breaking step >, and ⁇ mechanical treatment > were carried out in the same manner as that of Example 1, and thereafter, the polymerization degree of the obtained crosslink-broken phosphorylated cellulose fibers, and the supernatant yield, haze, viscosity, urethane bond amount, phosphoric acid group amount, crosslinked structure content of the obtained ultrafine fibrous cellulose-containing slurry, were measured according to the after-mentioned methods.
  • Example 2 Thereafter, the ⁇ sheet formation > was carried out in the same manner as that of Example 1, and the obtained ultrafine fibrous cellulose-containing sheet was measured according to the after-mentioned methods, in terms of tensile strength and YI values before and after heating.
  • Crosslink-broken phosphorylated cellulose fibers, ultrafine fibrous cellulose-containing slurry, and an ultrafine fibrous cellulose-containing sheet were obtained in the same manner as that of Example 1, with the exception that the pH of the pulp slurry was adjusted to be pH 10 in the ⁇ crosslink-breaking step > of Example 1.
  • the ultrafine fibrous cellulose-containing slurry supernatant yield, haze, viscosity, the amount of urethane bonds, and the content of crosslinked structures were measured according to the after-mentioned methods.
  • tensile strength and YI values before and after heating were measured according to the after-mentioned methods.
  • Crosslink-broken phosphorylated cellulose fibers, ultrafine fibrous cellulose-containing slurry, and an ultrafine fibrous cellulose-containing sheet were obtained in the same manner as that of Example 1, with the exceptions that HCl was used instead of NaOH and the pH of the pulp slurry was adjusted to be pH 4.0 in the ⁇ crosslink-breaking step > of Example 1.
  • HCl was used instead of NaOH
  • the pH of the pulp slurry was adjusted to be pH 4.0 in the ⁇ crosslink-breaking step > of Example 1.
  • supernatant yield, haze, viscosity, the amount of urethane bonds, and the content of crosslinked structures were measured according to the after-mentioned methods.
  • With regard to the ultrafine fibrous cellulose-containing sheet tensile strength and YI values before and after heating were measured according to the after-mentioned methods.
  • Crosslink-broken phosphorylated cellulose fibers, ultrafine fibrous cellulose-containing slurry, and an ultrafine fibrous cellulose-containing sheet were obtained in the same manner as that of Example 1, with the exceptions that HCl was used instead of NaOH and the pH of the pulp slurry was adjusted to be pH 1.0 in the ⁇ crosslink-breaking step > of Example 1.
  • HCl was used instead of NaOH
  • the pH of the pulp slurry was adjusted to be pH 1.0 in the ⁇ crosslink-breaking step > of Example 1.
  • supernatant yield, haze, viscosity, the amount of urethane bonds, and the content of crosslinked structures were measured according to the after-mentioned methods.
  • With regard to the ultrafine fibrous cellulose-containing sheet tensile strength and YI values before and after heating were measured according to the after-mentioned methods.
  • Phosphorylated cellulose fibers, ultrafine fibrous cellulose-containing slurry, and an ultrafine fibrous cellulose-containing sheet were obtained in the same manner as that of Example 1, with the exceptions that the heating time in the ⁇ crosslinking step > was set at 80 seconds, and further that the ⁇ crosslink-breaking step > was not carried out.
  • the ultrafine fibrous cellulose-containing slurry supernatant yield, haze, viscosity, the amount of urethane bonds, and the content of crosslinked structures were measured according to the after-mentioned methods.
  • the ultrafine fibrous cellulose-containing sheet tensile strength and YI values before and after heating were measured according to the after-mentioned methods.
  • Phosphorylated cellulose fibers, ultrafine fibrous cellulose-containing slurry, and an ultrafine fibrous cellulose-containing sheet were obtained in the same manner as that of Example 1, with the exception that the ⁇ crosslink-breaking step > was not carried out.
  • the ultrafine fibrous cellulose-containing slurry supernatant yield, haze, viscosity, the amount of urethane bonds, and the content of crosslinked structures were measured according to the after-mentioned methods.
  • the ultrafine fibrous cellulose-containing sheet tensile strength and YI values before and after heating were measured according to the after-mentioned methods.
  • Phosphorylated cellulose fibers, ultrafine fibrous cellulose-containing slurry, and an ultrafine fibrous cellulose-containing sheet were obtained in the same manner as that of Example 1, with the exception that the ⁇ crosslinking step > and ⁇ crosslink-breaking step > were not carried out.
  • the ultrafine fibrous cellulose-containing slurry supernatant yield, haze, viscosity, the amount of urethane bonds, and the content of crosslinked structures were measured according to the after-mentioned methods.
  • ultrafine fibrous cellulose-containing sheet tensile strength and YI values before and after heating were measured according to the after-mentioned methods.
  • a supernatant yield after completion of centrifugation was measured according to the following method.
  • the supernatant yield obtained after the centrifugation is used as an indicator of the yield of the ultrafine fibrous cellulose.
  • the higher the supernatant yield the higher the yield of the ultrafine fibrous cellulose that can be obtained.
  • Haze is a scale of the transparency of the ultrafine fibrous cellulose-containing slurry. The lower the haze value, the higher the transparency that can be achieved.
  • the haze of the ultrafine fibrous cellulose-containing slurry was measured by diluting the ultrafine fibrous cellulose-containing slurry after completion of the mechanical treatment step (fibrillation step) with ion exchange water to a concentration of 0.2% by mass, then placing the ultrafine fibrous cellulose-containing slurry into a glass cell for liquid having an optical path length of 1 cm (MG-40, manufactured by Fujiwara Scientific Company Co., Ltd., inverse optical path), and then measuring the haze thereof using a haze meter (HM-150, manufactured by MURAKAMI COLOR RESEARCH LABORATORY Co., Ltd.) in accordance with JIS K 7136. It is to be noted that the measurement of zero point was carried out with ion exchange water filled in the same glass cell as that described above.
  • the amount of phosphoric acid groups introduced was measured by a conductometric titration method. Specifically, fibrillation was carried out by a mechanical treatment step (fibrillation step), the obtained ultrafine fibrous cellulose-containing slurry was then treated with an ion exchange resin, and a change in the electrical conductivity was then obtained while adding a sodium hydroxide aqueous solution, thereby measuring the amount of phosphoric acid groups introduced.
  • a strongly acidic ion exchange resin (Amberjet 1024: conditioning agent, manufactured by Organo Corporation) was added to slurry containing 0.2% by mass of the ultrafine fibrous cellulose, and the resultant mixture was then shaken for 1 hour. Then, the mixture was poured onto a mesh having 90 ⁇ m-apertures to separate the resin from the slurry.
  • the change in the electric conductivity value indicated by the dispersion was measured while adding a 0.1 N aqueous solution of sodium hydroxide to the slurry containing fibrous cellulose after the ion exchange.
  • This conductometric titration confers a curve shown in Figure 1 as an alkali is added.
  • the electrical conductivity is rapidly reduced (hereinafter, this region is referred to as a "first region”).
  • the conductivity starts rising slightly (hereinafter, this region is referred to as a "second region”).
  • the increment of the conductivity is increased (hereinafter, this region is referred to as a "third region”).
  • three regions appear.
  • the boundary point between the second region and the third region is defined as a point at which the secondary differential value of conductivity, that is, the change in the increment (gradient) of conductivity becomes maximum.
  • the amount of the alkali required for the first region among these regions is equal to the amount of a strongly acidic group in the slurry used in the titration
  • the amount of the alkali required for the second region is equal to the amount of a weakly acidic group in the slurry used in the titration.
  • the amount (mmol) of the alkali required for the first region in the curve shown in Figure 1 was divided by the solid content (g) in the dispersion as a titration target to obtain the amount of the first dissociation alkali (mmol/g), and this amount was defined as the amount of phosphoric acid groups introduced.
  • the crosslinked structures are formed as a result of dehydration condensation performed by phosphoric acid groups that have been introduced into cellulose fibers. That is, it is a structure in which a glucose unit of cellulose binds to each of two P atoms of pyrophosphoric acid via an O atom. Accordingly, if crosslinked phosphoric acid groups are formed, weakly acidic groups are apparently lost, and as a result, the amount of alkali necessary for the second region is reduced in comparison to the amount of alkali necessary for the first region in Figure 1 .
  • the amount of the crosslinked structures are equal to a value obtained by dividing a difference between the amount of alkali necessary for the first region (first dissociation alkali amount) and the amount of alkali necessary for the second region (second dissociation alkali amount) by 2.
  • the ultrafine fibrous cellulose-containing slurry was diluted to a solid concentration of 0.4% by mass, and was then stirred using a disperser at 1500 rpm for 5 minutes.
  • the viscosity of the obtained slurry was measured using a type B viscometer (analog viscometer T-LVT, manufactured by BROOKFIELD). The measurement conditions were set to be 3 rpm and 25°C.
  • the content of the groups having a urethane bond was determined by measuring the amount of nitrogen covalently bound to cellulose. Specifically, after ionic nitrogen (ammonium ions) had been released and removed, the amount of nitrogen was measured according to a trace nitrogen analysis method. The release of ionic nitrogen (ammonium ions) was carried out under conditions where nitrogen covalently bound to cellulose was not substantially removed. The removal of the released ammonium ions was carried out by the same method as the measurement of the amount of phosphoric acid groups introduced. Specifically, the removal was carried out by adsorbing ammonium ions on a strongly acidic ion exchange resin.
  • the measurement was carried out using the trace total nitrogen analyzer TN-110, manufactured by Mitsubishi Chemical Analytech Co., Ltd. Before performing the measurement, a solvent was removed by drying a sample at a low temperature (for example, at 40°C for 24 hours in a vacuum dryer).
  • c indicates the concentration of the ultrafine fibrous cellulose at the time of measuring the viscosity.
  • this polymerization degree is an average polymerization degree measured according to viscometry, it is also referred to as a "viscosity average polymerization degree.”
  • the tensile strength and the tensile elastic modulus of the ultrafine fibrous cellulose-containing sheet were measured in accordance with JIS P 8113, using a tensile tester Tensilon (manufactured by A & D Co., Ltd.).
  • a test piece was prepared by humidity conditioning for 24 hours at 23°C and a relative humidity of 50%.
  • heating conditions were set to be 200°C, 4 hours, and vacuum drying.
  • ⁇ YI YI 2 ⁇ YI 1
  • YI 1 indicates yellowness before performing vacuum drying at 200°C for 4 hours
  • YI 2 indicates yellowness after performing vacuum drying at 200°C for 4 hours. Yellowness is a value measured in accordance with JIS K 7373.
  • Conditions for step (B) Amount of phosphoric acid groups / crosslink structures Amount of phosphoric acid groups after step (C) [mmol/g] Supernatant yield [%] Haze of slurry [%] Viscosity of slurry [mPa ⁇ s] Crosslink-breaking treatment pH After step (A) After step (B) Crosslink-breaking percentage (%) in step (B) Amount of alkali of first dissociation (amount of phosphoric acid groups) [mmol/g] Amount of alkali of second dissociation [mmol/g] Crosslinked structures [mmol/g] Amount of alkali of first dissociation (amount of phosphoric acid groups) [mmol/g] Amount of alkali of second dissociation [mmol/g] A
  • the yield of the ultrafine fibrous cellulose was high.
  • the obtained ultrafine fibrous cellulose-containing slurry had high transparency and high viscosity.
  • yellowness was suppressed in the obtained ultrafine fibrous cellulose-containing sheets.

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Claims (14)

  1. Procédé de production de cellulose fibreuse ayant une largeur de fibre de 1000 nm ou moins, comprenant :
    une étape consistant à introduire des groupes acide phosphorique (A), dans lequel (A) est composé de deux étapes :
    l'étape (a1) consistant à introduire des groupes acide phosphorique dans des fibres de cellulose en laissant un réactif de phosphorylation réagir avec une matière première de fibres comprenant de la cellulose en présence d'urée et/ou d'un dérivé de celle-ci,
    l'étape (a2) consistant à former des structures réticulées par l'intermédiaire des groupes acide phosphorique, de manière à obtenir des fibres de cellulose phosphorylées réticulées,
    dans lequel, dans l'étape (A) consistant à introduire des groupes acide phosphorique, un traitement thermique est effectué à une température de 100°C à 300°C.
    (B) rompre une partie ou de la totalité des structures réticulées pour obtenir des fibres de cellulose phosphorylées rompues par réticulation, et
    (C) effectuer un traitement mécanique sur les fibres de cellulose phosphorylées rompues par réticulation pour obtenir une cellulose fibreuse ayant une largeur de fibre de 1000 nm ou moins, dans lequel dans (A), des structures réticulées en une quantité de 0,05 mmol/g ou plus et de 2,0 mmol/g ou moins sont formées, et l'étape (B) consiste à effectuer l'hydrolyse des structures réticulées dans un solvant aqueux de pH 3 ou plus à une température de 80°C ou plus.
  2. Procédé de production de cellulose fibreuse selon la revendication 1, dans lequel, dans le (B), 50 % en moles ou plus des structures réticulées sont rompues.
  3. Procédé de production de cellulose fibreuse selon la revendication 1 ou 2, dans lequel le (B) est un traitement alcalin à chaud, dans lequel le solvant aqueux avec une valeur de pH supérieure à 7 est traité à une température de 80°C ou plus.
  4. Procédé de production de cellulose fibreuse selon l'une quelconque des revendications 1 à 3, dans lequel le degré de polymérisation des fibres de cellulose est mesuré selon Tappi T230, et dans lequel, lorsque le degré de polymérisation des fibres de cellulose avant d'être soumises à l'étape (A) est défini comme DPa et le degré de polymérisation des fibres de cellulose phosphorylées rompues par réticulation obtenues dans l'étape (B) est défini comme DPb, la valeur DPb/DPa est de 0,65 ou plus et de 0,94 ou moins.
  5. Procédé de production de cellulose fibreuse selon l'une quelconque des revendications 1 à 4, dans lequel le degré de polymérisation des fibres de cellulose est mesuré selon Tappi T230, dans lequel le degré de polymérisation (DPb) des fibres de cellulose phosphorylées rompues par réticulation obtenues dans le (B) est de 600 ou plus.
  6. Procédé de production de cellulose fibreuse selon l'une quelconque des revendications 1 à 5, dans lequel le degré de polymérisation des fibres de cellulose est mesuré selon le Tappi T230, dans lequel le degré de polymérisation (DPc) de la cellulose fibreuse ayant une largeur de fibre de 1000 nm ou moins obtenue dans le (C) est de 390 ou plus.
  7. Procédé de production de cellulose fibreuse selon l'une quelconque des revendications 1 à 6, dans lequel le réactif de phosphorylation est choisi dans le groupe constitué d'acide phosphorique, de sel d'acide phosphorique, de condensat déshydraté d'acide phosphorique, de sel de condensat déshydraté d'acide phosphorique, de pentoxyde de phosphore et d'oxychlorure de phosphore, ou un mélange de ceux-ci.
  8. Procédé de production de cellulose fibreuse selon l'une quelconque des revendications 1 à 7, dans lequel l'urée et/ou un dérivé de celle-ci est choisi dans le groupe constitué d'urée, de biuret, de 1-phényl urée, de 1-benzyl urée, de 1-méthyl urée et de 1-éthyl urée.
  9. Cellulose fibreuse obtenue par le procédé selon l'une quelconque des revendications 1 à 8 ayant une largeur de fibre de 1000 nm ou moins, qui ont des groupes acide phosphorique, dans laquelle
    la quantité des groupes acide phosphorique dans la cellulose fibreuse est de 1,65 mmol/g ou plus, et le degré de polymérisation mesuré selon Tappi T230 de la cellulose fibreuse est de 390 ou plus, et
    la cellulose fibreuse comprend des structures réticulées formées par les groupes acide phosphorique.
  10. Cellulose fibreuse selon la revendication 9, dans laquelle la teneur en groupes ayant une liaison uréthane est de 0,3 mmol/g ou moins.
  11. Bouillie comprenant la cellulose fibreuse selon la revendication 9 ou 10.
  12. Bouillie selon la revendication 11, ayant une viscosité à 25°C de 9500 mPa.s ou plus, dans laquelle la viscosité de la bouillie ayant une concentration de la cellulose fibreuse ultrafine de 0,4% en masse est mesurée en utilisant un viscosimètre de type B, un viscosimètre analogique T-LVT, fabriqué par BROOKFIELD à 25°C et 3 tr/min.
  13. Feuille comprenant la cellulose fibreuse selon la revendication 9 ou 10.
  14. Feuille selon la revendication 13, dans laquelle la valeur YI indiquant le jaunissement de la feuille est mesurée selon la norme JIS K 7373, dans laquelle la valeur YI obtenue après que la feuille ait été séchée sous vide à 200°C pendant 4 heures est définie comme YI2, et la valeur YI obtenue avant que la feuille soit séchée sous vide à 200°C pendant 4 heures est définie comme YI1, la valeur ΔYI représentée par YI2-YI1 est de 20 ou moins.
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TWI667270B (zh) * 2014-05-26 2019-08-01 日商王子控股股份有限公司 微細纖維及含微細纖維片的製造方法、由其得到的片及積層樹脂的樹脂複合體
WO2016002689A1 (fr) 2014-06-30 2016-01-07 王子ホールディングス株式会社 Composition contenant de minuscules fibres de cellulose
KR102106815B1 (ko) 2015-09-17 2020-05-06 오지 홀딩스 가부시키가이샤 미세 섬유상 셀룰로오스 함유물
JP6613771B2 (ja) * 2015-09-30 2019-12-04 王子ホールディングス株式会社 微細繊維状セルロース含有物
JP6569482B2 (ja) 2015-11-06 2019-09-04 王子ホールディングス株式会社 地下層処理用組成物、地下層処理用流体、地下層処理用流体の製造方法及び地下層の処理方法
JP7095595B2 (ja) 2016-02-19 2022-07-05 王子ホールディングス株式会社 繊維状セルロース含有物及び繊維状セルロース含有物の製造方法
CA3050730A1 (fr) 2016-03-31 2017-10-05 Oji Holdings Corporation Procede de production de cellulose fibreuse et cellulose fibreuse

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CA3019292A1 (fr) 2017-10-05
JP2018199826A (ja) 2018-12-20
CA3019292C (fr) 2019-08-27
EP3438132A1 (fr) 2019-02-06
US11111631B2 (en) 2021-09-07
JP2019090050A (ja) 2019-06-13
US20190127915A1 (en) 2019-05-02
WO2017170908A1 (fr) 2017-10-05
JPWO2017170908A1 (ja) 2018-04-05
EP3438132A4 (fr) 2019-12-11
JP2021036048A (ja) 2021-03-04
JP6394775B2 (ja) 2018-09-26
US10662585B2 (en) 2020-05-26
JP6252719B1 (ja) 2017-12-27
KR20180132757A (ko) 2018-12-12
CN109071681B (zh) 2020-03-13
US20200208350A1 (en) 2020-07-02
CA3050730A1 (fr) 2017-10-05
CN109071681A (zh) 2018-12-21
JP6791281B2 (ja) 2020-11-25
JP6512356B2 (ja) 2019-05-15
KR102050714B1 (ko) 2019-12-02

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